JP2012523471A - Method for producing terpolymers based on VDF, TRFE and CFE or CTFE - Google Patents

Method for producing terpolymers based on VDF, TRFE and CFE or CTFE Download PDF

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JP2012523471A
JP2012523471A JP2012504061A JP2012504061A JP2012523471A JP 2012523471 A JP2012523471 A JP 2012523471A JP 2012504061 A JP2012504061 A JP 2012504061A JP 2012504061 A JP2012504061 A JP 2012504061A JP 2012523471 A JP2012523471 A JP 2012523471A
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ボエ，フランソワ
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ピエゾテック
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F14/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
    • C08F14/18—Monomers containing fluorine
    • C08F14/22—Vinylidene fluoride
    • C—CHEMISTRY; METALLURGY
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    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
    • C08F214/18—Monomers containing fluorine
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
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    • C08F214/22—Vinylidene fluoride
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    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
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    • C08F214/26—Tetrafluoroethene
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    • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms

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Abstract

【課題】、ラジカル重合開始剤の存在下でＶＤＦ（二フッ化ビニリデン）と、ＴｒＦＥ（トリフルオロエチレン）と、ＣＦＥ（1−クロロ-1-フルオロ−エチレン）またはＣＴＦＥ（クロロトリフルオロエチレン）とのモノマーを重合してターポリマーを製造する方法。
【解決手段】下記(i)~(iv)を特徴とする方法：(i)ＣＦＥとＣＴＦＥとを含まない、ＶＤＦとＴｒＦＥとの初期混合物をオートクレーブ中に供給し、(ii)水にと混合した開始剤をオートクレーブ中に注入し、オートクレーブ内部の圧力を少なくとも80バールにしてＶＤＦとＴｒＦＥモノマーとの水中懸濁液を形成し、(iii)ＶＤＦとＴｒＦＥとＣＦＥまたはＣＴＦＥとから成る二次混合物をオートクレーブに注入し、(iv)重合反応が開始したら上記二次混合物を反応器に連続的に再注入し、反応器内部の圧力を少なくとも80バールの一定圧力に維持する。VDF (vinylidene difluoride), TrFE (trifluoroethylene), CFE (1-chloro-1-fluoro-ethylene) or CTFE (chlorotrifluoroethylene) in the presence of a radical polymerization initiator A method for producing a terpolymer by polymerizing monomers.
A method characterized by the following (i) to (iv): (i) An initial mixture of VDF and TrFE not containing CFE and CTFE is fed into an autoclave, and (ii) mixed with water. The initiator was injected into the autoclave, the pressure inside the autoclave was at least 80 bar to form a suspension in water of VDF and TrFE monomer, and (iii) a secondary mixture of VDF and TrFE and CFE or CTFE Is injected into the autoclave, and (iv) when the polymerization reaction starts, the secondary mixture is continuously reinjected into the reactor and the pressure inside the reactor is maintained at a constant pressure of at least 80 bar.

Description

本発明は、ＶＤＦ（二フッ化ビニリデン）と、ＴｒＦＥ（トリフルオロエチレン）と、ＣＦＥ（１−クロロ−１−フルオロ−エチレン）またはＣＴＦＥ（クロロトリフルオロエチレン）とのモノマーをラジカル重合開始剤の存在下で重合してターポリマーを製造する方法に関するものである。   In the present invention, monomers of VDF (vinylidene difluoride), TrFE (trifluoroethylene), CFE (1-chloro-1-fluoro-ethylene) or CTFE (chlorotrifluoroethylene) are used as radical polymerization initiators. The present invention relates to a method for producing a terpolymer by polymerization in the presence.

本発明方法で得られたターポリマーはリラクサ（relaxors）で且つ電歪性(electostrictive) であるといった特殊な特性を有する。従って、このターポリマーはアクチュエータ装置、マイクロポンプまたはコンデンサの製造で使用できる。   The terpolymer obtained by the method of the present invention has special properties such as relaxors and electrostrictive. This terpolymer can therefore be used in the manufacture of actuator devices, micropumps or capacitors.

本発明のターポリマーはさらに拡散相転移（diffuse phase transition）、極めて狭いヒステリシスループ、室温での高誘電率および比較的高い歪みを有する。
本発明のポリマーの室温での誘電率は少なくとも５０であり、電界誘電の分極は少なくとも０．１Ｃ／ｍ2と高く、破壊電界値で表される電気抵抗は４００ＭＶ／ｍ以下と優れ、それによって電気エネルギー貯蔵密度は３５０ＭＶ／ｍで少なくとも１０ Ｊ／ｃｍ3と高く、電気縦歪みは１７０ ＭＶ／ｍで７％に達する。 The terpolymers of the present invention further have a diffuse phase transition, a very narrow hysteresis loop, a high dielectric constant at room temperature and a relatively high strain.
The dielectric constant of the polymer of the present invention at room temperature is at least 50, the electric field dielectric polarization is as high as at least 0.1 C / m 2, and the electric resistance expressed by the breakdown electric field value is excellent at 400 MV / m or less, The electrical energy storage density is as high as at least 10 J / cm 3 at 350 MV / m, and the electrical longitudinal strain reaches 7% at 170 MV / m.

このタイプのコポリマーは特許文献１（欧州特許第１，７４８，０５３号公報）に記載の方法で製造されている。この方法はモノマー間の重合反応を開始する開始剤の存在下でオートクレーブ内で実施される。従って、この文献に記載の方法は、少なくとも３つのモノマー、例えば二フッ化ビニリデン（ＶＤＦ）およびトリフルオロエチレン（ＴｒＦＥ）と、これら２つのモノマーより反応性が高い少なくとも一種の他のモノマーとを含むコポリマーの製造に関するものである。   This type of copolymer is produced by the method described in Patent Document 1 (European Patent No. 1,748,053). This process is carried out in an autoclave in the presence of an initiator that initiates the polymerization reaction between the monomers. Thus, the method described in this document includes at least three monomers, such as vinylidene difluoride (VDF) and trifluoroethylene (TrFE), and at least one other monomer that is more reactive than these two monomers. It relates to the production of copolymers.

この方法は下記の段階を含む：
（ａ）反応性モノマーが少ない上記３つの構成モノマーの混合物を所定の反応容量中に供給し、
（ｂ）反応が開始したら、反応性が最も高いモノマーを多く含む各構成モノマーの混合物を一定圧力で連続的に再注入する（上記混合物の組成は周知な方法によって計算で求める）。 This method includes the following steps:
(A) supplying a mixture of the above three constituent monomers with less reactive monomer into a predetermined reaction volume;
(B) When the reaction starts, a mixture of constituent monomers containing a large amount of the most reactive monomer is continuously reinjected at a constant pressure (the composition of the mixture is calculated by a well-known method).

本発明者の行ったテストでは、上記方法には多くの欠点があることが観察された。特に、得られたコポリマーの特性を再現できないことがあるということが観察された。すなわち、上記方法の第２段階で行う再注入は重合反応開始後にしか行われず、しかも、反応の開始相の時間は不正確かつ不規則であることが観察された。   In tests conducted by the inventors, it has been observed that the above method has a number of drawbacks. In particular, it has been observed that the properties of the resulting copolymer may not be reproducible. That is, it was observed that the reinjection performed in the second stage of the above method was performed only after the initiation of the polymerization reaction, and that the reaction initiation phase time was inaccurate and irregular.

さらに、他のモノマーより反応性が高いモノマー、例えばＣＦＥが初期供給物の混合物中に存在するため、反応の開始相が時間とともに減速する傾向があることが観察された。   In addition, it was observed that the starting phase of the reaction tends to slow over time because monomers that are more reactive than the other monomers, such as CFE, are present in the initial feed mixture.

さらに、上記方法で重合を実施すると反応器の汚染度が高く、反応器の壁および得られたコポリマー粉末の両方に外皮（crusts）および表皮（skins）が存在することが観察された。重合温度が高いとこの現象はさらに顕著になり、大きな分子量を有するポリマーは得るのが難しい。反応器の壁および粉末中の両方でのこの汚染 (fouling) は下記の０〜３の４つのレベルのスケールで評価される：   Furthermore, it has been observed that when the polymerization is carried out in the manner described above, the reactor is highly contaminated and crusts and skins are present on both the reactor wall and the resulting copolymer powder. This phenomenon becomes more remarkable when the polymerization temperature is high, and it is difficult to obtain a polymer having a large molecular weight. This fouling both in the reactor wall and in the powder is evaluated on a four level scale from 0 to 3 as follows:

レベル０：
（１）反応器を空にし、水噴射で単純洗浄した後に反応器は清浄である。
（２）樹脂は外皮または表皮を全く含まない。
レベル１：
（１）反応器の壁の一部に脆い皮膜が存在する。
（２）撹拌器スピンドル上のわずかな塗膜または皮膜ができる。
（３）温度計ウェルは清浄。
（４）粉末には凝集体または塊が全くあるいはほとんどない。
レベル２：
（１）反応器の壁の大部分に脆くない硬い皮膜が存在する。
（２）撹拌器スピンドルが汚染または外皮で覆われる。
（３）温度計ウェル上に塗膜。
（４）粉末に凝集体および外皮の破片。
レベル３：
（１）反応器の表面の大部分に厚い抵抗塗膜の存在する。
（２）撹拌器スピンドルが強固な外皮で覆われる。
（３）温度計ウェルの周囲にブロックおよびフィラメント。
（４）粉末に多数の表皮および外皮の存在。 Level 0 :
(1) The reactor is clean after emptying and simple washing with water jet.
(2) The resin does not contain any skin or epidermis.
Level 1 :
(1) A brittle film is present on part of the reactor wall.
(2) A slight film or film is formed on the agitator spindle.
(3) The thermometer well is clean.
(4) The powder has no or almost no aggregates or lumps.
Level 2 :
(1) A hard coating that is not brittle exists on most of the walls of the reactor.
(2) The stirrer spindle is covered with contamination or skin.
(3) Coating film on thermometer well.
(4) Agglomerates and skin debris in powder.
Level 3 :
(1) A thick resistive coating is present on most of the reactor surface.
(2) The stirrer spindle is covered with a strong skin.
(3) Blocks and filaments around the thermometer well.
(4) Presence of numerous epidermis and outer skin in the powder.

上記方法に従って重合した重合体の汚染レベルを上記のスケールを用いて評価すると上記レベル１、２、３が付くが、本発明の方法で製造したものは常にレベル０となり、再現性もある。   When the contamination level of the polymer polymerized according to the above method is evaluated using the above scale, the above levels 1, 2, and 3 are attached, but those produced by the method of the present invention always have level 0 and are reproducible.

欧州特許第１，７４８，０５３号公報European Patent 1,748,053

本発明の目的は上記公知方法の欠点を克服することにある。   The object of the present invention is to overcome the drawbacks of the known methods.

上記目的は、本発明に従ってラジカル重合開始剤の存在下で下記（１）〜（３）のモノマーを懸濁重合してターポリマーを製造する方法で達成される：
（１）ＶＤＦ（二フッ化ビニリデン）モノマー、
（２）ＴｒＦＥ（トリフルオロエチレン）モノマー、
（３）ＣＦＥ（１−クロロ−１−フルオロエチレン）またはＣＴＦＥ（クロロトリフルオロエチレン）モノマー。 The above object is achieved by a method for producing a terpolymer by suspension polymerization of the following monomers (1) to (3) in the presence of a radical polymerization initiator according to the present invention:
(1) VDF (vinylidene difluoride) monomer,
(2) TrFE (trifluoroethylene) monomer,
(3) CFE (1-chloro-1-fluoroethylene) or CTFE (chlorotrifluoroethylene) monomer.

本発明方法は下記の段階を含むことを特徴とする：
（ｉ）ＣＦＥとＣＴＦＥとを含まない、ＶＤＦとＴｒＦＥとの初期混合物をオートクレーブ中に供給し、
（ｉｉ）水に混合した開始剤をオートクレーブ中に注入し、オートクレーブ内部の圧力を少なくとも８０バールにしてＶＤＦとＴｒＦＥモノマーとの水中懸濁液を形成し、
（ｉｉｉ）ＶＤＦとＴｒＦＥとＣＦＥまたはＣＴＦＥとで構成される二次混合物をオートクレーブに注入し、
（ｉｖ）重合反応が開始したら、上記の二次混合物を反応器に連続的に再注入し、反応器内部の圧力を少なくとも８０バールの一定圧力に維持する。 The method according to the invention is characterized in that it comprises the following steps:
(I) supplying an initial mixture of VDF and TrFE without CFE and CTFE into an autoclave;
(Ii) injecting an initiator mixed with water into the autoclave and forming a suspension in water of VDF and TrFE monomer under an autoclave internal pressure of at least 80 bar;
(Iii) injecting a secondary mixture composed of VDF and TrFE and CFE or CTFE into the autoclave;
(Iv) Once the polymerization reaction has started, the above secondary mixture is continuously reinjected into the reactor and the pressure inside the reactor is maintained at a constant pressure of at least 80 bar.

本発明の製造方法を実施する設備の一つの例を示す図。本発明を限定するものではない。The figure which shows one example of the equipment which enforces the manufacturing method of this invention. It is not intended to limit the invention.

初期混合物は下記の重量組成を有するのが有利である：
（１）ＶＤＦの比率が２５〜９５％、好ましくは５５〜８０％である、
（２）ＴｒＦＥの比率が５〜７５％、好ましくは２０〜４５％である。 The initial mixture advantageously has the following weight composition:
(1) The ratio of VDF is 25 to 95%, preferably 55 to 80%.
(2) The ratio of TrFE is 5 to 75%, preferably 20 to 45%.

二次混合物は下記の重量組成を有する：
（１）ＶＤＦの比率が２０〜８０％、好ましくは３５〜７０％である、
（２）ＴｒＦＥの比率が３〜６０％、好ましくは１４〜４０％である、
（３）ＣＦＥまたはＣＴＦＥの比率が４〜６７％、好ましくは７〜３４％である。 The secondary mixture has the following weight composition:
(1) The ratio of VDF is 20 to 80%, preferably 35 to 70%.
(2) The ratio of TrFE is 3 to 60%, preferably 14 to 40%.
(3) The ratio of CFE or CTFE is 4 to 67%, preferably 7 to 34%.

初期混合物と二次混合物との重量比は０．４〜２である。
本発明方法を用いることで、上記の公知方法で得られたターポリマーの特性より高い特性を有するターポリマーを再現性良く得ることができる。
さらに、本発明方法の実施ははるかに簡単である。これは特に、不正確でしかも不規則である反応開始相の時間に依存しないことによる。
さらに、表皮または外皮を含まない高分子量のターポリマーが粉末の形で得られる。 The weight ratio of the initial mixture to the secondary mixture is 0.4-2.
By using the method of the present invention, a terpolymer having characteristics higher than those of the terpolymer obtained by the above-mentioned known method can be obtained with good reproducibility.
Furthermore, the implementation of the method of the invention is much simpler. This is in particular because it is not dependent on the time of the initiating phase, which is inaccurate and irregular.
Furthermore, a high molecular weight terpolymer free of epidermis or skin is obtained in powder form.

オートクレーブ内部圧力は８０〜１１０バールにし、温度は４０℃〜６０℃に維持するのが好ましい。
ＶＤＦとＴｒＦＥとＣＦＥまたはＣＴＦＥとの二次混合物は、例えば逆止め弁を組込んだゲートを介してをオートクレーブ中に連続的に再注入する。二次混合物は２つの直列に連結したコンプレッサを用いて圧縮した後、オートクレーブ中に再注入することができる。二次混合物は、オートクレーブ中の圧力より高い圧力下すなわち８０バール以上の値でオートクレーブ中に注入する。 The autoclave internal pressure is preferably 80-110 bar and the temperature is preferably maintained at 40-60 ° C.
A secondary mixture of VDF and TrFE and CFE or CTFE is continuously reinjected into the autoclave, for example through a gate incorporating a check valve. The secondary mixture can be re-injected into the autoclave after being compressed using two serially connected compressors. The secondary mixture is injected into the autoclave under a pressure higher than that in the autoclave, i.e. above 80 bar.

本発明方法で得られたターポリマーは、ｘモル％のＶＤＦと、ｙモル％のＴｒＦＥと、（１００−ｘ−ｙ）モル％のＣＦＥまたはＣＴＦＥとで構成される。
ここで、
ｘは３０〜８０、好ましくは４０〜７０であり、
ｙは５〜６０、好ましくは２０〜５０であり、
ｘとｙとの合計は８０〜９７、好ましくは９０〜９５である。 The terpolymer obtained by the method of the present invention is composed of x mol% VDF, y mol% TrFE, and (100-xy) mol% CFE or CTFE.
here,
x is 30 to 80, preferably 40 to 70,
y is 5-60, preferably 20-50,
The sum of x and y is 80 to 97, preferably 90 to 95.

例えば、得られたターポリマーは６１．８モル％のＶＤＦと、２９．８モル％のＴｒＦＥと、８．５モル％のＣＦＥとで構成される。
本発明方法を用いると、平均分子量が４００ ０００以上（粘度測定法で測定）のターポリマーを得ることができる。本発明のターポリマーは外皮または表皮を全く含まない。
本発明の上記以外の特徴および利点は以下の詳細な説明からより良く理解できよう。 For example, the resulting terpolymer is composed of 61.8 mol% VDF, 29.8 mol% TrFE, and 8.5 mol% CFE.
When the method of the present invention is used, a terpolymer having an average molecular weight of 400,000 or more (measured by a viscosity measuring method) can be obtained. The terpolymers of the present invention do not contain any skin or epidermis.
Other features and advantages of the present invention will be better understood from the following detailed description.

図１に示した設備は基本的にオートクレーブ１と、これに設けられた撹拌器２と、加熱マントル３と、サーモスタット４とを備える。オートクレーブ１は例えば内側容積が４リットルである。このオートクレーブ１には複数の管、例えば真空ポート管５、初期気体混合物導入管６、開始剤注入管７および二次気体混合物注入用およびこの混合物の再注入用の管８が接続されている。   The equipment shown in FIG. 1 basically includes an autoclave 1, a stirrer 2 provided on the autoclave 1, a heating mantle 3, and a thermostat 4. The autoclave 1 has an inner volume of 4 liters, for example. Connected to the autoclave 1 are a plurality of tubes, for example, a vacuum port tube 5, an initial gas mixture introduction tube 6, an initiator injection tube 7, and a secondary gas mixture injection tube 8 and a tube 8 for reinjecting the mixture.

管６は一つのシリンダまたは２つの独立したシリンダ、それぞれＶＤＦおよびＴｒＦＥを約２〜３バールの圧力下に含むシリンダに接続するためのものである。
管７は加圧ポンプ９に接続され、このポンプによって一定量の開始剤１０をオートクレーブ１に注入できる。
管８はシリンダ１１または複数の独立したシリンダ、それぞれＶＤＦ、ＴｒＦＥおよびＣＦＥを約２〜３バールの圧力下に含むシリンダに接続するためのものである。 Tube 6 is for connecting to one cylinder or two independent cylinders, each containing VDF and TrFE under a pressure of about 2-3 bar.
The pipe 7 is connected to a pressurizing pump 9 by which a certain amount of initiator 10 can be injected into the autoclave 1.
The tube 8 is for connecting to a cylinder 11 or a plurality of independent cylinders, each containing VDF, TrFE and CFE under a pressure of about 2-3 bar.

シリンダ１１と管８との間には、２つのコンプレッサ１２、１３が直列で接続されている。このコンプレッサはシリンダ１１から出てくる気体を圧縮し、この気体をオートクレーブ１に注入または再注入するためのものである。
参照番号１４、１５、１６、１７は圧力を表示する圧力計を示す。
上記設備を用いた本発明方法の一つの実施例は以下の手順に従って行う。 Two compressors 12 and 13 are connected in series between the cylinder 11 and the pipe 8. This compressor is for compressing the gas coming out of the cylinder 11 and injecting or reinjecting this gas into the autoclave 1.
Reference numerals 14, 15, 16, and 17 denote pressure gauges that display pressure.
One embodiment of the method of the present invention using the above equipment is performed according to the following procedure.

段階（ｉ）
ＶＤＦとＴｒＦＥとの初期混合物をオートクレーブ１に管６を介して導入する。一つの実施例では、この供給物は４６３．３４ｇのＶＤＦおよび２８６．６６ｇのＴｒＦＥ、すなわち６７．４３モル％のＶＤＦおよび３２．５７モル％のＴｒＦＥで構成される。 Stage (i)
An initial mixture of VDF and TrFE is introduced into the autoclave 1 via a tube 6. In one example, the feed is composed of 463.34 g VDF and 286.66 g TrFE, ie 67.43 mol% VDF and 32.57 mol% TrFE.

段階（ｉｉ）
開始剤１０はペルオキシジカルボネートファミリのラジカル開始剤である。この開始剤は管７を介してオートクレーブ１に注入される。
オートクレーブ１に導入される水によって、このオートクレーブの内部を８０バール以上、好ましくは８０〜１００バールの圧力下に置く。
オートクレーブ１に入れた２種のモノマーが臨界相に達したら、これらを水中懸濁液中に入れる。 Stage (ii)
Initiator 10 is a radical initiator of the peroxydicarbonate family. This initiator is injected into the autoclave 1 via the tube 7.
With the water introduced into the autoclave 1, the interior of the autoclave is placed under a pressure of 80 bar or more, preferably 80-100 bar.
When the two monomers in autoclave 1 reach the critical phase, they are placed in a suspension in water.

段階（ｉｉｉ）
一つまたは複数のシリンダ１１に入れたＶＤＦとＴｒＦＥとＣＦＥとの二次混合物を、２つのコンプレッサ１２、１３によって過圧し、管８および、逆止め弁を備えたゲート１８を介してオートクレーブ１に注入する。
上記の二次混合物を、オートクレーブ１の内部の８０バールよりわずかに高い圧力、好ましくは８０バール以上、１１０バール以下の範囲でオートクレーブ１に注入する。 Stage (iii)
A secondary mixture of VDF, TrFE, and CFE in one or more cylinders 11 is over-pressurized by two compressors 12 and 13, and enters the autoclave 1 through a pipe 8 and a gate 18 equipped with a check valve. inject.
The secondary mixture is injected into the autoclave 1 at a pressure slightly higher than 80 bar inside the autoclave 1, preferably in the range of 80 bar to 110 bar.

二次混合物の組成は、例えば６０６ｇのＶＤＦ、３７４．９２ｇのＴｒＦＥ、および１５．４６ｇのＣＦＥ、すなわち５７．０１モル％のＶＤＦ、２７．５３モル％のＴｒＦＥおよび１５．４６モル％のＣＦＥである。
オートクレーブ１の内部温度は４５℃〜５２℃の値に維持する。
次いで、３種のモノマー間の重合反応を開始する。重合の結果、水中懸濁液中のモノマーが固体粉末に変換され、圧力降下が生じる。この圧力降下によって、一つまたは複数のシリンダ１１に入れた３種のモノマーの混合物が自動的にオートクレーブ１に連続的且つ一定圧力で再注入される。 The composition of the secondary mixture is, for example, 606 g VDF, 374.92 g TrFE, and 15.46 g CFE, ie 57.01 mol% VDF, 27.53 mol% TrFE and 15.46 mol% CFE. is there.
The internal temperature of the autoclave 1 is maintained at a value of 45 ° C to 52 ° C.
Next, a polymerization reaction between the three monomers is started. As a result of the polymerization, the monomer in the suspension in water is converted to a solid powder and a pressure drop occurs. Due to this pressure drop, a mixture of three monomers in one or more cylinders 11 is automatically reinjected into the autoclave 1 continuously and at a constant pressure.

重合プロセスを約５時間続ける。この間、オートクレーブ１の内部圧力は８０バール以上の値、好ましくは８０〜１００バールの間の値に維持される。同様に、温度は４５℃〜５２℃に維持される。
モノマーのターポリマーへの変換収率は約８０〜９０％である。
洗浄および乾燥後に得られたターポリマーは表皮を含まない白色粉末の形である。得られたターポリマーは下記のモル組成を有する：
ＶＤＦ： ６１．７０％
ＴｒＦＥ：２９．８０％
ＣＦＥ： ８．５０％ The polymerization process is continued for about 5 hours. During this time, the internal pressure of the autoclave 1 is maintained at a value of 80 bar or higher, preferably between 80 and 100 bar. Similarly, the temperature is maintained between 45 ° C and 52 ° C.
The conversion yield of monomer to terpolymer is about 80-90%.
The terpolymer obtained after washing and drying is in the form of a white powder without epidermis. The resulting terpolymer has the following molar composition:
VDF: 61.70%
TrFE: 29.80%
CFE: 8.50%

得られたターポリマーの平均分子量は４１３，０００である。これは溶剤としてメチルエチルケトンを用いて粘度測定法によって２０℃で測定した。
この分子量はオートクレーブの温度を５２℃以上の値に設定することによって、この値より大きくすることができる。
上記実施例はＣＦＥをＣＴＦＥに替えて繰り返すことができる。 The average molecular weight of the obtained terpolymer is 413,000. This was measured at 20 ° C. by a viscosity measurement method using methyl ethyl ketone as a solvent.
This molecular weight can be made larger than this value by setting the autoclave temperature to a value of 52 ° C. or higher.
The above embodiment can be repeated by replacing CFE with CTFE.

Claims (12)

下記（ｉ）〜（ｉｖ）の段階を含むことを特徴とする、ラジカル重合開始剤の存在下でＶＤＦ（二フッ化ビニリデン）と、ＴｒＦＥ（トリフルオロエチレン）と、ＣＦＥ（１−クロロ−１−フルオロ−エチレン）またはＣＴＦＥ（クロロトリフルオロエチレン）とのモノマーを重合してターポリマーを製造する方法：
（ｉ）ＣＦＥとＣＴＦＥとを含まない、ＶＤＦとＴｒＦＥとの初期混合物をオートクレーブ中に供給し、
（ｉｉ）オートクレーブ中に水に混合した開始剤を注入し、オートクレーブ内部の圧力を少なくとも８０バールにしてＶＤＦとＴｒＦＥモノマーとの水中懸濁液を形成し、
（ｉｉｉ）オートクレーブ中にＶＤＦとＴｒＦＥとＣＦＥまたはＣＴＦＥとから成る二次混合物を注入し、
（ｉｖ）重合反応が開始したら、上記の二次混合物を反応器中に連続的に再注入し、反応器内部の圧力を少なくとも８０バールの一定圧力に維持する。 VDF (vinylidene difluoride), TrFE (trifluoroethylene), and CFE (1-chloro-1) in the presence of a radical polymerization initiator, comprising the following steps (i) to (iv): A method for producing a terpolymer by polymerizing monomers with -fluoro-ethylene) or CTFE (chlorotrifluoroethylene):
(I) supplying an initial mixture of VDF and TrFE without CFE and CTFE into an autoclave;
(Ii) injecting an initiator mixed in water into the autoclave and setting the pressure inside the autoclave to at least 80 bar to form a suspension in water of VDF and TrFE monomer;
(Iii) injecting a secondary mixture of VDF and TrFE and CFE or CTFE into the autoclave;
(Iv) Once the polymerization reaction has started, the above secondary mixture is continuously reinjected into the reactor and the pressure inside the reactor is maintained at a constant pressure of at least 80 bar. 上記初期混合物の組成を下記にする請求項１に記載の方法：
（１）ＶＤＦの比率を２５〜９５％、好ましくは５５〜８０％にし、
（２）ＴｒＦＥの比率を５〜７５％、好ましくは２０〜４５％にする。 The method of claim 1, wherein the composition of the initial mixture is:
(1) VDF ratio is 25 to 95%, preferably 55 to 80%,
(2) The ratio of TrFE is 5 to 75%, preferably 20 to 45%. 上記二次混合物の重量組成を下記にする請求項１または２に記載の方法：
（１）ＶＤＦの比率を２０〜８０％、好ましくは３５〜７０％にし、
（２）ＴｒＦＥの比率を３〜６０％、好ましくは１４〜４０％にし、
（３）ＣＦＥまたはＣＴＦＥの比率を４〜６７％、好ましくは７〜３４％にする。 The method according to claim 1 or 2, wherein the weight composition of the secondary mixture is as follows:
(1) VDF ratio is 20 to 80%, preferably 35 to 70%,
(2) The ratio of TrFE is 3 to 60%, preferably 14 to 40%,
(3) The ratio of CFE or CTFE is 4 to 67%, preferably 7 to 34%. （ｉｉ）〜（ｉｖ）段階でのオートクレーブ内部の圧力を少なくとも８０バールにする請求項１〜３のいずれか一項に記載の方法。   The method according to any one of claims 1 to 3, wherein the pressure inside the autoclave in steps (ii) to (iv) is at least 80 bar. オートクレーブ内部の温度を４０℃〜６０℃の値に維持する請求項１〜４のいずれか一項に記載の方法。   The method as described in any one of Claims 1-4 which maintains the temperature inside an autoclave at the value of 40 to 60 degreeC. ＶＤＦとＴｒＦＥとＣＦＥまたはＣＴＦＥとの二次混合物をオートクレーブ中に逆止め弁を有するゲートを介して連続的に再注入する請求項１〜５のいずれか一項に記載の方法。   6. The method according to any one of claims 1 to 5, wherein the secondary mixture of VDF and TrFE and CFE or CTFE is continuously reinjected into the autoclave through a gate having a check valve. 二次混合物を直列な２つのコンプレッサを用いて圧縮した後にオートクレーブ中に再注入する請求項１〜６のいずれか一項に記載の方法。   7. A process according to any one of the preceding claims, wherein the secondary mixture is compressed using two compressors in series and then reinjected into the autoclave. 得られたターポリマーがｘモル％のＶＤＦと、ｙモル％のＴｒＦＥと、（１００−ｘ−ｙ）モル％のＣＦＥまたはＣＴＦＥとで構成される（ここで、ｘは３０〜８０、好ましくは４０〜７０であり、ｙは５〜６０、好ましくは２０〜５０であり、ｘとｙとの合計は８０〜９７、好ましくは９０〜９５である）請求項１〜７のいずれか一項に記載の方法。   The resulting terpolymer is composed of x mol% VDF, y mol% TrFE, and (100-xy) mol% CFE or CTFE, where x is 30-80, preferably 8) to 70, y is 5 to 60, preferably 20 to 50, and the sum of x and y is 80 to 97, preferably 90 to 95). The method described. 得られたターポリマーが６１．８モル％のＶＤＦと、２９．８モル％のＴｒＦＥと、８．５モル％のＣＦＥとで構成される請求項８に記載の方法。   The method of claim 8, wherein the resulting terpolymer is composed of 61.8 mol% VDF, 29.8 mol% TrFE, and 8.5 mol% CFE. 得られたターポリマーの平均分子量が４００ ０００以上である請求項１〜９のいずれか一項に記載の方法。   The average molecular weight of the obtained terpolymer is 400,000 or more, The method as described in any one of Claims 1-9. アクチュエータ装置、マイクロポンプまたはコンデンサの製造で上記ターポリマーを用いる段階を含む請求項１〜１０のいずれか一項に記載の方法。   11. A method according to any one of the preceding claims, comprising using the terpolymer in the manufacture of an actuator device, micropump or capacitor. ｘモル％のＶＤＦと、ｙモル％のＴｒＦＥと、（１００−ｘ−ｙ）モル％のＣＦＥまたはＣＴＦＥとで構成され（ここで、ｘは３０〜８０、好ましくは４０〜７０であり、ｙは５〜６０、好ましくは２０〜５０であり、ｘとｙとの合計は８０〜９７、好ましくは９０〜９５である）、粉末の形で得られ、外皮または表皮を含まない請求項１〜１１のいずれか一項に記載の方法で得られるターポリマー。   x mol% VDF, y mol% TrFE and (100-xy) mol% CFE or CTFE (where x is 30-80, preferably 40-70, y 5 to 60, preferably 20 to 50, and the sum of x and y is 80 to 97, preferably 90 to 95), obtained in the form of a powder and does not contain an outer skin or epidermis A terpolymer obtained by the method according to any one of 11.
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FR2944285B1 (en) 2011-11-25
US20140135464A1 (en) 2014-05-15
EP2417169B1 (en) 2015-09-23
US8552127B2 (en) 2013-10-08
WO2010116105A1 (en) 2010-10-14
US9290587B2 (en) 2016-03-22
US20120116039A1 (en) 2012-05-10
CN102803315A (en) 2012-11-28
FR2944285A1 (en) 2010-10-15
KR101682077B1 (en) 2016-12-02
KR20110138231A (en) 2011-12-26
JP5611320B2 (en) 2014-10-22
CN102803315B (en) 2014-10-22

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